[0001] The invention relates to a method for preparing hard polyurethane and polyisocyanurate
foams, wherein an isocyanate and an active hydrogen containing compound, such as a
polyol, are made to react in the presence of a catalyst, a foam stabilizer and a blowing
agent which contains chloropropane.
[0002] The use of chloropropane, on laboratory scale, as blowing agent for the polyurethane
foam production, has already been mentioned in Belgian patent No.656.018 of Mobay
Chemical Company.
[0003] However, it appeared that when manufacturing such a foam on an industrial scale by
using chloropropane as blowing agent, an important shrinkage is observed especially
for foams having the most usual densities of about 30 kg/m³. In a rather unexpected
way, it has been determined that such a shrinkage cannot be observed on laboratory
scale, such as it is the case in said Belgian patent.
[0004] Consequently, an object of the invention is to remedy this important drawback for
the manufacturing of polyurethane foams and/or polyisocyanate foams on an industrial
or semi-industrial scale.
[0005] To this end, use is made of a foam stabilizer being mainly of the non silicon type.
[0006] Suitably, this non silicon based foam stabilizer is formed by at least one copolymer
having following general structural formula :

wherein :
- A is a cyclic or acyclic group having :
1 to 12 carbon atoms
2 to [26-(j+m)] hydrogen atoms,
0 to 4 oxygen atoms,
0 to 2 nitrogen atoms,
- E is a group having as general structual formula :

wherein n = 3 to 5,
- G is a group having as general structural formula :
-C
uH
2y-2(̵

- O C
vH
2v+1)̵₂
wherein u = 2 or 3
v = 2 to 9,
- K is a group having as structural formula :
R-, R-CO-, RNHCO-, ROC(CH₃)H-,

wherein R is an acyclic or cyclic radical having 1 to 18 carbon atoms and X = 3 or
4,
wherein further : j = 0 to 8
m = 0 to 4
1 ≦ j + m ≦ 8
s = 2 to 4
w = 1 to 200
p = 1 to 10
q = 1 to 10
r = 1 to 50.
[0007] In another embodiment of the invention, use is made of non silicon based foam stabilizers
of the non ionic, anionic and/or cationic type, such as defined in claims 4 to 6.
[0008] In a more particular embodiment of the invention, substantially only non silicon
based components are used as foam stabilizers.
[0009] Other particularities and advantages of the invention will become apparent from the
following more detailed description wherein some specific examples of the method for
preparing polyurethane foam and polysicyanurate foam according to the invention are
described ; this description is only given by way of example and does not limit the
scope of the invention.
[0010] For the production of these polyurethane foams, use is essentially made of the reaction
between a polyalcohol and an isocyanate in the presence of the appropriate catalysts.
[0011] Beside the polyisocyanate, the polyols, the typical catalysts and the blowing agents,
use is furthermore made of foam stabilizers, fire retardant additives, etc.
[0012] The organic polyisocyanate compounds are of the R(NCO)
n type, wherein n > 2 and R represents an aliphatic or aromatic group. Preferably,
use is made of diisocyanates or polyisocyanates, having an average of 2 to 4 isocyanate
groups per molecule. A typical example hereof is diphenylmethane-4,4′-diisocyanate
(MDI) and mixtures of the latter with its polymeric forms ("crude" MDI), which are
usually applied in the rigid polyurethane foam or polyisocyanate foam manufacture.
In certain cases, use can also be made of prepolymerized forms of MDI.
[0013] In principle, each molecule containing active hydrogen groups such as : R-OH, R-COOH,
R-SH, R₂-NH, R-NH₂, R-SH, ...can serve as reaction substrate. Preferably, there is
started from polyalcohols of the polyetherpolyol or the polyesterpolyol type or mixtures
thereof. (Polyetherpolyols, based on aromatic chain initiators, are furthermore preferred).
[0014] A molecular weight of at least 150,and preferably between 500 and 5000, is typical.
The functionality is always higher or equal to 2 and a hydroxyl number (IOH) comprised
between 25 and 1000 being an important characteristic.
[0015] For the polyurethane preparation, use is made of an isocyanate with an index approaching
the stoechiometric ratio, i.e. 95 à 110, whereas the polyisocyanurate preparation
requires a much higher index in order to allow the trimerization reaction of the isocyanate
as such. This isocyanate index is usually higher than 150.
[0016] In order to obtain the typical foam structure, use is made of a chemical or physical
blowing agent. Usually H₂O, which liberates "in situ" CO₂ by reaction with isocyanate,
is applied as chemical blowing agent. As physical blowing agents, low boiling organic
liquids are used, which evaporate as a result of the urea, urethane and trimerisation
reactions and contribute to the formation of the typical foam structure.
[0017] Chloro-fluoro-hydrocarbon compounds (CFK's) are commonly used as physical blowing
agents such as for example trichlorofluoromethane, trichlorotrifluoroethane, dichlorotrifluoroethane,
dichlorofluoromethane, or other analogous compounds or combinations thereof.
[0018] In this invention, a considerably fraction of the CFK's or the totality of the latters
is replaced by chloropropane. Also other blowing agents, such as for example pentane,
isopentane, etc..., mixed with chloropropane, can be used. The total blowing agent
amount which is used, is dependent upon the foam density to be obtained and the molecular
weight of the blowing agent. Amounts between 1 and 50 % by weight and preferably between
1 and 30 % by weight, are typical.
[0019] Contrary to the teachings of the Mobay patent, an excess of non silicon based cell
stabilizers is used here, preferably without the presence of the classic, silicon
based cell stabilizers. As it appears from the examples, it is impossible to manufacture,
with these classic substances and on an industrial scale, foams which are dimensionally
stable, especially in the low density range around 30 kg/m³. Foam stabilizers of the
non silicon type are for example described in US patent No. 4.091.030 of Air Products
and Chemicals, Inc. These foam stabilizers are copolymers having as general structural
formula :

wherein :
- A is a cyclic or acyclic group having :
1 to 12 carbon atoms
2 to [26-(j+m)] hydrogen atoms,
0 to 4 oxygen atoms,
0 to 2 nitrogen atoms,
- E is a group having as general structual formula :

wherein n = 3 to 5,
- G is a group having as general structural formula :
-C
uH
2y-2(̵

- O C
vH
2v+1)̵₂
wherein u = 2 or 3
v = 2 to 9,
- K is a group having as structural formula :
R-, R-CO-, RNHCO-, ROC(CH₃)H-,

wherein R is an acyclic or cyclic radical having 1 to 18 carbon atoms and X = 3 or
4,
wherein further : j = 0 to 8
m = 0 to 4
1 ≦ j + m ≦ 8
s = 2 to 4
w = 1 to 200
p = 1 to 10
q = 1 to 10
r = 1 to 50.
[0020] An example of such a compound is the molecule wherein group E is N-vinyl-2-pyrrolidinone
and group G is dibutylmaleate. These compounds are used in the present invention under
their brand names LK221 and LK443. Preferably amounts of 0.1-10 parts by weight and
more specifically 0.1 to 4 parts by weight are used per 100 parts by weight polyol.
[0021] Other examples of non ionic, non silicon stabilizers are :
- condensation products of alkylphenols with ethylene oxide having as general structural
formula :

wherein R comprises 8 to 14 C atoms and x varies from 1 to 40
- mono-, di- or tri-esters of condensation products of sorbitan with ethylene oxide.Preferably
laurate, palmitate, stearate or oleate esters are used.
- condensation products of fatty acids with ethylene oxide, such as for example the
condensation products of stearic acid with ethylene oxide ;
- condensation products of alcohols with ethylene oxide, with a hydrophobic chain
containing usually 12 to 18C atoms and being condensed with (n-3) moles ethylene oxide
(n indicating the number of C atoms of the hydrophobic chain) ;
- condensation products of amides with ethylene oxide, such as for example the diethanolamine
monostearate derivative condensed with 2 moles ethylene oxide ;
- condensation products of amines with ethylene oxide, such as for example the products
starting from oleylamine and ethylene oxide ;
- condensation products of mercaptane derivatives and ethylene oxide ;
- acetylene derivatives, such as for example the product having as structural formula
:

condensed with 0 to 40 moles ethylene oxide.
[0022] Besides the non ionic stabilizers, also anionic or cationic stabilizers are appropriate.
The following compounds can be mentioned for use as anionic components :
ROSO₃
⊖M
⊕
R₂OSO₃
⊖M
⊕
R-SO₃
⊖M
⊕
R-

-OSO₃
⊖M
⊕
C₇F₁₅COO
⊖NH₄
⊕

(φ)
x-CH₂SO₄
⊖M
⊕
wherein R is an alkyl radical having 8 to 20 C atoms and wherein M⁺ represents a counterion,
such as for example H⁺, K⁺, Na⁺, NR₄⁺, NH₄⁺,....
[0023] These compounds can comprise furthermore also condensation chains with ethylene
oxide.
[0024] Important, appropriate cationic components are :
- amines in the shape of acetate or chlorohydrate
- quaternary ammonium salts
- pyridine and quinoline derivatives
- derivatives of ethanolamines.
[0025] As catalyst, use is made of tertiary amine compounds, such as for example N,N′-dimethylcyclohexylamine,
diaminobicyclo-octane (DABCO), etc..., or metal , alkali metal or alkaline-earth metal
salts of organic or anorganic origin, such as for example potassium octoate, dibutyltin
dilaurate, Fomrez UL 28 (Trademark of Witco), Sn-mercaptides, etc...
[0026] The amounts which are used here are dependent on the catalytic activity and are typically
comprised between 0.01 and 10 parts by weight, and more specifically between 0.01
and 4 parts by weight, per 100 parts by weight polyol.
[0027] Extra additives, such as for example fire retardants (phosphor and halogen containing
additives or polyols), smoke suppressors, additional cross-linkers, fillers, diluents
, etc.., can always be added in order to give the final product certain specific features.
[0028] This invention allows the production of foams either according to a continuous process,
or according to a discontinuous process and as well in the shape of whether or not
coated plates as in the shape of blocks, in situ moulded pieces or spayed foam.
[0029] The physical properties (and the respective norm) which have been measured for the
hard foams, are grouped in Table 1.

[0030] In order to allow a sufficiently quick evaluation of the λ value under real conditions,
use is made here of a fastened aging method.
[0031] The λ value is measured after the manufacturing of the foam, as well as in function
of the time, the samples being conditioned at 70°C during a time period untill 15
weeks after the manufacturing. This λ value is a stabilized value and can be correlated
with the long term, final insulating value of the foam under actual application circumstances.
[0032] The use of 2-chloropropane is illustrated in the following examples.
Examples 1 - 9
[0033] In these examples, the replacement of Freon 11 (Trademark of Du Pont) by 2-chloropropane
is illustrated in a conventional polyurethane system. At the same time, the effect
of the cell stabilizer is emphasized here.
[0034] There has been started from a polyol based on an aliphatic initiator. The hydroxyl
number of this polyol was 520 mg KOH/g polyol. For the isocyanate, there has been
started from a "crude" MDI having an equivalent weight of 135. The isocyanate index
was 110. The formulations are shown in Table 2. The foams have been prepared on a
laboratorium scale, the mixture of polyol, blowing agent, catalyst, stabilizer and
water having been mixed very intensively during about 10 seconds with the isocyanate
at about 4000 revolutions per minute. The foaming mixture is then poured in a receptacle
with dimensions : 30 x 30 x 20 cm.
[0035] The physical properties of the foams prepared in examples 1 - 9 are given in Table
3.
Table 2
formulations as used in examples 1 - 9 |
Example |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
Composition : |
|
|
|
|
|
|
|
|
|
Polyol : XZ 95203.00 (1) |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
100 |
Trichloroethylfosfate |
10 |
10 |
10 |
10 |
10 |
10 |
10 |
10 |
10 |
Silicon - Stabilizer B 1903(2) |
1.2 |
1.2 |
- |
1.2 |
- |
1.2 |
- |
1.2 |
- |
Non silicon - Stabilizer LK 221 (3) |
- |
- |
1.2 |
- |
1.2 |
- |
1.2 |
- |
1.2 |
Water |
1.2 |
1.2 |
1.2 |
1.2 |
1.2 |
1.2 |
1.2 |
1.2 |
1.2 |
Dimethylcyclohexylamine |
3.0 |
3.0 |
3.0 |
2.8 |
2.9 |
2.9 |
2.8 |
2.9 |
2.8 |
Freon (4) |
40 |
30 |
30 |
20 |
20 |
10 |
10 |
- |
- |
2-chloropropane |
- |
5.2 |
5.2 |
10.5 |
15.8 |
15.8 |
15.8 |
21 |
21 |
MDI 44V40 (5) |
157 |
157 |
157 |
157 |
157 |
157 |
157 |
157 |
157 |
(1) A Dow chemical trademark |
(2) A Th. Goldschmidt AG trademark |
(3) An Air Products trademark |
(4) A du Pont trademark |
(5) A Bayer trademark |
Table 3
Physical properties of the foams manufactured in examples 1-9. |
Example |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
Physical property |
|
|
|
|
|
|
|
|
|
Core density (kg/m³) |
29,8 |
29.2 |
29.4 |
29.6 |
29.2 |
29.6 |
28.9 |
29.1 |
29.3 |
Hardness (kPa) |
152 |
137 |
148 |
162 |
141 |
132 |
162 |
153 |
151 |
Closed cells (%) |
93.1 |
92.6 |
93.8 |
93.7 |
92.7 |
91.9 |
94.2 |
94.0 |
92.8 |
Friability (%) |
6.8 |
6.2 |
5.9 |
4.9 |
5.0 |
4.1 |
4.2 |
2.9 |
3.2 |
Dimens. stability (%) |
<3 |
<3 |
<3 |
<3 |
<3 |
<3 |
<3 |
<3 |
<3 |
Shrinkage at 4°C (%) |
1.2 |
3.2 |
1.4 |
9 |
1.1 |
6.3 |
1.5 |
7.1 |
1.4 |
Fire class (ASTM D 1692) |
S.E.* |
S.E. |
S.E. |
S.E. |
S.E. |
S.E. |
S.E. |
S.E. |
S.E. |
Fire class (DIN 4102) |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
LOI |
22.5 |
22.5 |
22.5 |
22 |
22 |
22.5 |
22 |
22 |
22 |
λ initial (W/mK) |
0.0200 |
0.0198 |
0.0194 |
0.0209 |
0.0205 |
0.0212 |
0.0215 |
0.0219 |
0.0220 |
λ after 15 w. 70°C (W/mK) |
0.0247 |
0.0245 |
0.0248 |
0.0252 |
0.0249 |
0.0256 |
0.0252 |
0.0258 |
0.0255 |
* S.E. : self extinguishing |
[0036] Table 3 shows clearly that the use of 2-chloropropane in combination with the non
silicon stabilizer results in foams having a shrinkage behaviour similar to traditional
foams based on CFC11, and this in contrast with these foams involving the application
of a silicon based surfactant. From these examples it appears furthermore that with
the ISO 2796 method no distinction can be made between the foams which are subject
to shrinkage and the stable foams. The shrinkage test at 4°C does indicate a clear
distinction. The foam as obtained in example 8 is a foam prepared according to the
method described in the Mobay patent No. 656.018 (1964). It will be clear that foams,
which are subject to such a shrinkage, are not industrializable. With the present
invention (example 9) it is on the contrary possible to manufacture a foam having
shrinkage properties comparable to a Freon 11 (a Du Pont trademark) blown foam. Further,
a rather small λ value increase (after 15 weeks at 70°C) seems to occur, compared
with the Freon 11 (a Du Pont trademark) blown foam. From these examples, it appears
furthermore that the fire classes of the foams manufactured on basis of 2-chloropropane,
do essentielly not differ from the Freon 11 (a Du Pont trademark) blown foam. There
has to be mentioned here that the λ values are relatively high since the samples have
been manufactured on a laboratory scale. In the next examples, the foams are manufactured
with a machine whereby the improved mixing causes a.o. an improvement of the cell
structure and thus also of the λ value. An important, addition advantage of 2-chloropropane
is the friability reduction at higher 2-chloropropane contents.
Example 10 - 15
[0037] In these examples, there has been started from polyols based on aliphatic as well
as on aromatic chain initiators and also from polyols being mixtures thereof.
[0038] The polyols have comparable hydroxyl numbers which are on average situated at about
530. In these examples, there has been started always from an isocyanate index of
110. Use has been made of 2-chloropropane as blowing agent. The applied formulations
are given in Table 4.
[0039] The foams have been manufactured in the shape of plates on a double belt machine.
A coated glass film of 300 g/m² has been applied as covering.
[0040] The physical properties of the obtained products are given in Table 5. From the latter
it appears clearly that the combined use of 2-chloropropane and a non silicon foam
stabilizer (in this case LK 443) results in a stable foam having a dimensional stability
(at 4°C) which is superior to all of the other cases. It has to be mentioned that
the stability has been evaluated here on the foam without the covering. From these
examples, it appears furthermore that the present invention is effective for any polyol,
independent of the nature of this polyol. In an analogous way as has been described
with respect to examples 1 - 9, there are obtained foams having a good λ aging behaviour.
Table 4
Formulations as used in examples 10-15. |
Example |
10 |
11 |
12 |
13 |
14 |
15 |
Composition : |
|
|
|
|
|
|
Polyol : XZ 95203.00 (1) |
100 |
100 |
- |
- |
- |
- |
Polyol Caradol MD 944 (2) |
- |
- |
100 |
100 |
- |
- |
Polyol Baymer VP PU 1504 (3) |
- |
- |
- |
- |
100 |
100 |
Dimethylmethylfosfonate |
6 |
6 |
8 |
8 |
- |
- |
Silicon Stabilizer B 1903 (4) |
1.5 |
- |
1.5 |
- |
1.5 |
- |
Non silicon Stabilizer LK 443 (5) |
- |
0.8 |
- |
0.8 |
- |
0.8 |
Water |
0.45 |
0.45 |
1 |
1 |
0.8 |
0.8 |
dimethylcyclohexylamine |
2.0 |
2.0 |
1.5 |
1.5 |
3.2 |
3.2 |
2-chloropropane |
26 |
26 |
26 |
26 |
26 |
26 |
MDI 44V40 (3) |
145 |
145 |
159 |
159 |
144 |
144 |
(1) A Dow Chemical trademark |
(2) A Shell trademark |
(3) A Bayer trademark |
(4) A Th. Goldschmidt AG trademark |
(5) An Air Products trademark. |
Table 5
Physical properties of the foams manufactured in examples 10-15. |
Example |
10 |
11 |
12 |
13 |
14 |
15 |
Physical property |
|
|
|
|
|
|
Core density (kg/m³) |
27.4 |
27.6 |
28.1 |
27.5 |
28.3 |
28.0 |
Hardness (kPa) |
162 |
174 |
187 |
161 |
171 |
163 |
Shrinkage at 4° C (%) |
8.3 |
1.5 |
6.8 |
1.2 |
6.9 |
1.3 |
Fire class ASTM D1692 |
S.E.(*) |
S.E. |
S.E. |
S.E. |
S.E. |
S.E. |
DIN 4201 (5) |
B3 |
B3 |
B2 |
B2 |
B2 |
B3 |
LOI ASTM D2863 |
23 |
22 |
25 |
24.5 |
24 |
24 |
Friability |
3.1 |
3.4 |
2.9 |
2.4 |
2.9 |
3.1 |
λ initial |
0.0189 |
0.0186 |
0.0172 |
0.0174 |
0.0180 |
0.0180 |
λ after 15 w 70°C |
0.0239 |
0.0241 |
0.0232 |
0.0237 |
0.0242 |
0.0236 |
(*) S.E. : self extinguishing |
Examples 16 - 22
[0041] In these examples, there are made large blocks with dimensions of 2 m x 0.60 m x
0.60 m. There has been started from mixtures wherein a combination of a sorbitol based
polyetherpolyol and a polyesterpolyol based on phosphorous acid have been applied.2-Chloropropane
has been used in each case as blowing agent, but at decreasing concentration so that
foam densities typically of 30 kg/m³ to 75 kg/m³ have been obtained. As isocyanate,
use has been made of a prepolymerized isocyanate having an equivalent weight of about
150.
[0042] The formulations are given in Table 6.
[0043] The physical properties are summed up in Table 7. It appears from the latter that
2-chloropropane can also be used for the manufacturing of blocks whereby densities
of 30-80 kg/cm³ can be obtained.
[0044] The advantage of 2-chloropropane in combination with the cell stabilizers as described
hereabove, resides in the fact that shrink-proof and stable foams are obtained which
present furthermore an excellent aging behaviour as a result of which the conductivity
coefficient remains relatively reduced in time.
Table 6
Formulations as used in examples 16-22. |
Example |
16 |
17 |
18 |
19 |
20 |
21 |
22 |
Composition |
|
|
|
|
|
|
|
Polyetherpolyol |
75 |
75 |
75 |
75 |
75 |
75 |
75 |
Polyesterpolyol |
25 |
25 |
25 |
25 |
25 |
25 |
25 |
LK 221 (*) |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
1.7 |
Diethylamine |
1.75 |
1.75 |
1.75 |
1.80 |
1.80 |
1.90 |
1.95 |
Sn octoaat |
0.05 |
0.05 |
0.05 |
0.05 |
0.05 |
0.05 |
0.05 |
K octoaat |
0.5 |
0.5 |
0.4 |
0.4 |
0.3 |
0.3 |
0.3 |
2-chloropropane |
22.2 |
19.2 |
16.8 |
15.0 |
12.3 |
10.2 |
7.9 |
Polymer MDI |
142 |
142 |
142 |
142 |
142 |
142 |
142 |
(*) An Air Products trademark. |
Table 7
Physical properties of the foams manufactured in examples 16-22 |
Example |
16 |
17 |
18 |
19 |
20 |
21 |
22 |
Physical property |
|
|
|
|
|
|
|
Core density (kg/m³) |
30.7 |
34.9 |
41.2 |
45.6 |
49.8 |
60.2 |
75.6 |
Hardness (kPA) |
152 |
182 |
264 |
292 |
330 |
483 |
634 |
Closed cells (%) |
91 |
91 |
90 |
92 |
92 |
91 |
91 |
Friability (%) |
14.7 |
12.8 |
12.4 |
10.2 |
9.2 |
8.7 |
6.0 |
Shrinkage at 4°C (%) |
1.3 |
0.9 |
0.5 |
0.4 |
0.4 |
0.2 |
0.2 |
λ initial (W/mK) |
0.0199 |
0.0208 |
0.0210 |
0.0207 |
0.0210 |
0.0215 |
0.0220 |
λ after 15 w 70°C (W/mK) |
0.0232 |
0.0239 |
0.0239 |
0.0244 |
0.0250 |
0.0249 |
0.0260 |
Fire test DIN 4102 |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
B3 |
LOI |
22 |
22 |
22 |
22 |
22 |
22 |
22 |
Examples 23 - 26
[0045] In these examples, a formulation analogous to the one described in example 14, has
been used. The foam has been manufactured in a discontinuous way, the reacting mixture
having been injected between two rigid coverings (steel and polyester plate). In this
example, four different thicknesses have been manufactured, a different densification
factor being applied, as shown in Table 8, dependent upon the thickness.
Table 8
Densification factors and densities as used in examples 23-26 |
Example |
23 |
24 |
25 |
26 |
Thickness (mm) |
60 |
90 |
160 |
200 |
Densification factor |
1.43 |
1.28 |
1.22 |
1.20 |
Core density (kg/cm³) |
42.4 |
41.0 |
38.9 |
38.2 |
[0046] The obtained panels present excellent mechanical properties. The bond of the polyurethane
to the coverings was similar to the one obtained in the cases wherein Freon 11 (a
Du Pont trademark) has been used.
Example 27
[0047] In this example, a formula having an isocyanate index of 250 has been used. There
has been started from a polyesterpolyol as shown in Table 9.
Table 9
Formulation as used in Example 27 |
Polyol Chardol 336 A (a) |
100 |
Non silicon stabilizer Fomrez M 66-82A (b) |
1.5 |
Catalyst TMR 30 (c) |
0.2 |
K octoate |
1.6 |
2-chloropropane |
16 |
MDI (44V20) (d) |
138 |
(a) A Chardanol trademark |
(b) A Witco trademark |
(c) An Air Products trademark |
(d) A Bayer trademark. |
[0048] The foams described in these examples have been manufactured on a machine by which
the two components (in this case a mixture of, on the one hand, polyol, catalyst,
cell stabilizer and MDI on the other hand) are mixed under high pressure in a mixing
chamber and subsequently spread out in a mould on a covering consisting mainly of
aluminium covered with a polyethylene layer. Afterwards, the mould has been closed
and opened again after about 5 minutes. In this way, foam plates of 40 cm x 40 cm
x 5 cm were obtained.
[0049] The physical properties of the foam are given in Table 10.
Table 10
Physical properties of the foam as manufactured in Example 27. |
Core density (kg/cm³) |
40 |
Hardness (kPa) |
250 |
Fire tests ASTM D1692 |
self extinguishing |
Fire test DIN 4102 |
B2 |
LOI |
25 |
Closed cells (%) |
92.7 |
Shrinkage at 4°C (%) |
1.8 |
λ initial |
0.0210 |
λ after 15 w. 70°C |
0.0249 |
[0050] From this table it appears that also polyisocyanurate foams can be manufactured by
means of this technology which are not any more subject to shrinkage.
Example 28
[0051] In this example, there has been started from a formulation which is mainly used in
spray applications. The formulation is given in Table 11.
Table 11
Formulation as used in Example 28 |
Polyol Acrol 3750 (*) |
34.2 |
Dibutyltindilaurate |
0.2 |
Stabilizer LK 443 (**) |
0.3 |
2-chloropropane |
8.6 |
Polymeric isocyanate |
50.9 |
(*) An Arco trademark |
(**) An Air Products trademark |
[0052] The foams showed a good insulation value (λ = 0.0190 W/mK) and an excellent aging
behaviour (λ after 15 weeks at 70°C = 0.0228 W/mK).
[0053] This example indicates that chloropropane, especially 2-chloropropane, can be used
as blowing agent in spray applications.
Examples 29 - 38
[0054] In these examples, foams have been manufactured which are analogous to the foam described
in Example 8. However, there has been started from a series of non silicon based stabilizers.
The used products are typical examples of the products as described hereabove. The
evaluation criterion was always the shrinkage determined at 4°C.

[0055] It appears that the shrinkage is always considerably smaller than the one obtained
in Example 8 (Table 3).
Example 39
[0056] In this example use has been made of 1-chloropropane as blowing agent. The foam has
been manufactured in a similar way as the one described in Example 18, the 2-chloropropane
being replaced by equal amounts of 1-chloropropane. The properties of this foam are
similar to the ones as given in Table 1.
1. A method for preparing hard polyurethane and polyisocyanurate foams wherein an
isocyanate and an active hydrogen containing compound are made to react in the presence
of a catalyst, a foam stabilizer and a blowing agent which contains chloropropane,
the used foam stabilizer being mainly of the non silicon type.
2. A method according to claim 1, characterized in that as foam stabilizer, use is
made of a non silicon based component which is formed by at least one copolymer having
following general structural formula :

wherein :
- A is a cyclic or acyclic group having :
1 to 12 carbon atoms
2 to [26-(j+m)] hydrogen atoms,
0 to 4 oxygen atoms,
0 to 2 nitrogen atoms,
- E is a group having as general structual formula :

wherein n = 3 to 5,
- G is a group having as general structural formula :
-C
uH
2y-2(̵

- O C
vH
2v+1)̵₂
wherein u = 2 or 3
v = 2 to 9,
- K is a group having as structural formula :
R-, R-CO-, RNHCO-, ROC(CH₃)H-,

wherein R is an acyclic or cyclic radical having 1 to 18 carbon atoms and X = 3 or
4,
wherein further : j = 0 to 8
m = 0 to 4
1 ≦ j + m ≦ 8
s = 2 to 4
w = 1 to 200
p = 1 to 10
q = 1 to 10
r = 1 to 50.
3. A method according to claim 2, characterized in that use is made of a copolymer
having above mentioned general structural formula, wherein A is a hydrocarbon radical
having 2 to 26-j hydrogen atoms and wherein m equals 0.
4. A method according to anyone of claims 1 to 3, characterized in that use is made
of non ionic, non silicon based foam stabilizers consisting at least of one of the
following components :
- condensation products of alkylphenols with ethylene oxide having as general structural
formula :

wherein R comprises 8 to 14 C atoms and x varies from 1 to 40
- -mono-, di- or tri-esters of condensation products of sorbitan with ethylene oxide,
use being preferably made of laurate, palmitate, stearate or oleate esters ;
- condensation products of fatty acids with ethylene oxide, such as for example the
condensation products of stearic acid with ethylene oxide ;
- condensation products of alcohols with ethylene oxide, with a hydrophobic chain
containing usually 12 to 18C atoms and being condensed with (n-3) moles ethylene oxide
(n indicating the number of C atoms of the hydrophobic chain) ;
- condensation products of amides with ethylene oxide, such as for example the diethanolamine
monostearate derivative condensed with 2 moles ethylene oxide ;
- condensation products of amines with ethylene oxide, such as for example the products
starting from oleylamine and ethylene oxide ;
- condensation products of mercaptane derivatives and ethylene oxide ;
- acetylene derivatives, such as for example the product having as structural formula
:

condensed with 0 to 40 moles ethylene oxide.
5. A method according to anyone of claims 1 to 3, characterized in that use is made
of anionic stabilizers consisting at least of one of following components :
ROSO₃
⊖M
⊕
R₂ OSO₃
⊖M
⊕
R-SO₃
⊖M
⊕
R-

-OSO₃
⊖M
⊕
C₇F₁₅CO
⊖NH₄
⊕

(φ)
x-CH₂SO₄
⊖M
⊕
wherein R is an alkyl radical having 8 to 20 C atoms and wherein M⁺ represents a counterion,
such as for example H⁺, K⁺, Na⁺, NR₄⁺, NH₄⁺,....
6. A method according to anyone of claims 1 to 3, characterized in that use is made
of cationic stabilizers consisting at least of one of following components :
- amines in the shape of acetate or chlorohydrate
- quaternary ammonium salts
- pyridine and quinoline derivatives
- derivates of ethanolamines.
7. A method according to anyone of claims 1 to 6, characterized in that substantially
only non silicon based components are used as foam stabilizers.
8. A method according to anyone of claims 1 to 7, characterized in that use is made
of 0.01 to 10 parts by weight, and preferably 0.1 to 4 parts by weight, of said foam
stabilizer per 100 parts by weight polyol.
9. A method according to anyone of claims 1 to 8, characterized in that a physical
blowing agent is used comprising mainly 2-chloropropane.
10. A method according to claim 9, characterized in that a physical blowing agent
is used comprising at least 90 %, and consisting preferably substantially completely
of chloropropane.